Systems and methods for removing sulfer and halogens

ABSTRACT

Provided herein are systems and methods for removing halogens and sulfur from used oil. The used oil is heated and aerated, followed by rapid vaporization and cooling. The cooled oil is then subjected to an electrical field before being filtered.

CROSS REFERENCE TO RELATED APPLICATION(S)

This application is a continuation of U.S. Ser. No. 14/589,640, filedJan. 5, 2015, now pending, which claims the benefit of priority under 35U.S.C. § 119(e) of U.S. Ser. No. 61/924,028, filed Jan. 6, 2014, theentire content of each of which is incorporated herein by reference.

BACKGROUND OF THE INVENTION Field of the Invention

The invention relates generally to used oil treatment and morespecifically to systems and methods for converting halogens in oil tosodium containing compounds for removal therefrom.

Background Information

Fossil fuels are the largest and most widely used source of power in theworld, offering high efficiency, proven performance, and relatively lowprices. There are many different types of fossil fuels, ranging frompetroleum fractions to coal, tar sands, and shale oil, with uses rangingfrom consumer uses such as automotive engines and home heating tocommercial uses such as boilers, furnaces, smelting units, and powerplants.

Fossil fuels and other crude oil fractions and products derived fromnatural sources contain a vast array of hydrocarbons differing widely inmolecular weight, boiling and melting points, reactivity, and ease ofprocessing. Many industrial processes have been developed to upgradethese materials by removing, diluting, or converting the heaviercomponents or those that tend to polymerize or otherwise solidify,notably the olefins, aromatics, and fused-ring compounds such asnaphthalenes, indanes and indenes, anthracenes, and phenanthracenes.

For fossil fuels in particular, a growing concern is the need to removesulfur compounds. Sulfur from sulfur compounds causes corrosion inpipeline, pumping, and refining equipment, the poisoning of catalystsused in the refining and combustion of fossil fuels, and the prematurefailure of combustion engines. Sulfur poisons the catalytic convertersused in diesel-powered trucks and buses to control the emissions ofoxides of nitrogen (NO_(x)). Sulfur also causes an increase inparticulate (soot) emissions from trucks and buses by degrading the soottraps used on these vehicles. The burning of sulfur-containing fuelproduces sulfur dioxide which enters the atmosphere as acid rain,inflicting harm on agriculture and wildlife, and causing hazards tohuman health.

Another growing concern in fossil fuels is total halogen content in usedoil. According to the U.S. Environmental Protection Agency (EPA), usedoil containing more than 1,000 ppm total halogens is presumed to be ahazardous waste because it has been mixed with a halogenated hazardouswaste. Since halogens form toxic compounds that have negative effects onhuman health and the environment, a need exists for methods andapparatus to efficiently remove such halogens from used oil.

SUMMARY OF THE INVENTION

The present invention is based on the finding that used oil can betreated for removal of halogen and/or sulfur content.

In one aspect, the invention provides a method of treating oil. Themethod includes heating oil that is inputted into the system, aeratingthe heated oil to create an oil foam, subjecting the oil foam to avacuum to condense the oil, cooling the condensed oil, contacting thecondensed oil with a sintered metal, subjecting the cooled oil to anelectrical field, and filtering the electrified oil. The oil may be usedoil. In various embodiments, the oil is heated to about 82° F.-100° F.In various embodiments, the temperature is raised to approximately 85°F.-90° F. In certain embodiments, the temperature is raised toapproximately 88° F. In various embodiments, the electrical field is a0-90 volt electrical field is produced through sintered copper. Invarious embodiments, the electrical field is a 0-250 volt electricalfield is produced through sintered titanium. The step of aerating mayinclude passing the oil through a plurality of nitrogen diffusers. Theoil may be cooled to about 72° F.-80° F. In various embodiments, thecooling chamber (90) cools the oil to approximately 72° F.-75° F. Incertain embodiments, the cooling chamber (90) cools the oil toapproximately 73° F. The filter bank may include a 1-20 micron filter.

In another aspect, the invention provides a system for treating oil. Thesystem includes a line for inputting oil, a heating coil having an inputand an output, wherein the input is in fluid communication with theline, and the heating coil is configured for heating the inputted oil,an air injection passage in fluid communication with the output of theheating coil, the air injection passage comprising a plurality ofsintered metal injectors configured to aerate the heated oil, a vacuumchamber in fluid communication with an output of the air injectionpassage, and configured to condense the aerated oil, a cooling chamberin fluid communication with an output of the vacuum chamber, andconfigured to cool the condensed oil, a chamber containing sinteredmetal in fluid communication with an output of the cooling chamber, anelectrifier in fluid communication with an output of the coolingchamber, and configured to subject the cooled oil to an electricalfield, and a filter bank in fluid communication with an output of theelectrifier, and configured to filter the electrified oil. The oil maybe used oil. In various embodiments, the heating coil may be configuredto heat the inputted oil to about 82° F.-100° F. In various embodiments,the heating coil may be configured to heat the inputted oil to about 85°F.-90° F. In certain embodiments, the heating coil may be configured toheat the inputted oil to about 88° F. In various embodiments, the airinjection passage comprises a plurality of nitrogen diffusers in contactwith the heated oil. The cooling chamber may be configured to cool theoil to about 72° F.-80° F. In various embodiments, cooling chamber maybe configured to cool the oil to about 72° F.-75° F. In certainembodiments, cooling chamber may be configured to cool the oil to about73° F. In various embodiments, the electrifier comprises sintered copperin contact with the condensed oil, and is configured to generate a 0-90volt electrical field through the sintered copper. In variousembodiments, the electrifier comprises sintered titanium in contact withthe condensed oil, and is configured to generate a 0-250 volt electricalfield through the sintered titanium. The filter bank may include a 1-20micron filter.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a pictorial diagram showing a halogen removal system.

FIG. 2 is a cross-sectional view of a vacuum column showing airinjection ports and nitrogen diffusers used to aerate the oil to formoil foam.

FIG. 3 is a pictorial diagram showing a pump for creating eddy current.

FIGS. 4A and 4B are perspective and cross-sectional views of a coolingchamber.

FIG. 5A is a pictorial diagram showing a cross-sectional view of anelectrifier containing a sintered metal.

FIG. 5B is a pictorial diagram showing the creation of atomic shellwobble as a result of subjecting the oil to an electric field.

FIG. 6 is a cross-sectional view of a gathering chamber.

DETAILED DESCRIPTION OF THE INVENTION

The present invention is based on the finding that used oil can betreated for removal of halogen and/or sulfur content.

Before the present compositions and methods are described, it is to beunderstood that this invention is not limited to particularcompositions, methods, and experimental conditions described, as suchcompositions, methods, and conditions may vary. It is also to beunderstood that the terminology used herein is for purposes ofdescribing particular embodiments only, and is not intended to belimiting, since the scope of the present invention will be limited onlyin the appended claims.

As used in this specification and the appended claims, the singularforms “a”, “an”, and “the” include plural references unless the contextclearly dictates otherwise. Thus, for example, references to “themethod” includes one or more methods, and/or steps of the type describedherein which will become apparent to those persons skilled in the artupon reading this disclosure and so forth.

The term “comprising,” which is used interchangeably with “including,”“containing,” or “characterized by,” is inclusive or open-ended languageand does not exclude additional, unrecited elements or method steps. Thephrase “consisting of” excludes any element, step, or ingredient notspecified in the claim. The phrase “consisting essentially of” limitsthe scope of a claim to the specified materials or steps and those thatdo not materially affect the basic and novel characteristics of theclaimed invention. The present disclosure contemplates embodiments ofthe invention compositions and methods corresponding to the scope ofeach of these phrases. Thus, a composition or method comprising recitedelements or steps contemplates particular embodiments in which thecomposition or method consists essentially of or consists of thoseelements or steps.

Unless defined otherwise, all technical and scientific terms used hereinhave the same meaning as commonly understood by one of ordinary skill inthe art to which this invention belongs. Although any methods andmaterials similar or equivalent to those described herein can be used inthe practice or testing of the invention, the preferred methods andmaterials are now described.

Used oil is any oil refined from crude oil or any synthetic oil that hasbeen used and as a result of such use is contaminated by physical orchemical impurities. Used oils include spent automotive lubricatingoils, spent industrial oils, and spent industrial process oils. Thus,the definition of used oil includes oil used for the purpose oflubrication that becomes contaminated as a result of such use andresidues and sludges derived from used oil.

The halogen family, or Group VIIA on the periodic table of elements,includes fluorine, chlorine, bromine, iodine, and astatine. Chemicalscontaining both a halogen atom and a carbon atom are called “organichalogens.” Examples of organic halogens include short chain alkanes like1,2-dichloroethane, hexachloroethane, and short chain (C10-C13)chlorinated paraffins. Chemicals containing an atom from the halogenfamily but no carbon atoms are “inorganic halogens.” Examples ofinorganic halogens include sodium chloride (table salt) and thalliumchloride. Total halogens include organic and inorganic halogens, exceptas noted in analytical procedures. EPA proposed regulating totalchlorine in used oil but finalized the regulatory term as “totalhalogens” after comments submitted in response to the proposed ruleindicated that most “total chlorine” analytical methods actually measurehalogens other than chlorine only.

Used oil handlers may determine whether the total halogen content isabove or below 1,000 ppm by (1) testing the used oil or (2) applyingknowledge of the halogen content of the used oil in light of thematerials or processes used. If testing to determine the total halogencontent of a used oil waste stream, handlers should properly sample andanalyze the used oil using a total halogen test method.

Referring to FIG. 1, an oil treatment system (500) is shown. The systemis configured to convert halogens back to sodium which are thencrystallized, captured and removed via a filter bank. Used oil entersthe system through a pipe (10) (denoted as “oil in”), and flows througha heating coil (20) where it is heated to approximately 82° F.-100° F.In various embodiments, the temperature is raised to approximately 85°F.-90° F. In certain embodiments, the temperature is raised toapproximately 88° F. From the heating coil, the oil passes through anair injection passage (30) of a vacuum column (103) where a plurality ofsintered metal air injectors (35) aerate the heated oil using alow-volume air compressor (37). As shown in FIG. 4, the air injectors(35) aerate the heated oil through nitrogen diffusers (42) connectedthereto, and produce uniform air bubbles (50) of approximately 1/32″diameter or less. In various embodiments, the uniform bubbles areapproximately 1/32″ in diameter. In various embodiments, the nitrogendiffusers (42) are formed from sintered brass. The resulting air bubblesform an oil foam (52) and provide for thin film exposure of the usedoil, thereby maximizing exposure of the oil to the electromagnetictreatment within the column (103). A vacuum is simultaneously applied tothe column (103) using a vacuum pump (45), resulting in rapid expansionand vaporization of the used oil as a result of artificial heat. Therapid vaporization reduces the surface tension of the oil foam, therebycreating a thinner bubble wall to speed up molecular movement. As theoil foam is exposed to the non-flooded portion of the vacuum tower(i.e., the controlled oil level at approximately mid-point of the vacuumchamber (40)), the bubbles rapidly expand and go into a violentvaporization state, thereby removing volatile organic compounds (VOCs)from the oil. These VOCs are thereafter captured in the vacuum pump (45)filtering system (not shown) prior to being exhausted to the atmosphere.In various embodiments, the vacuum chamber (103) is a tower that may beapproximately 15-20 feet high to allow for sufficient vaporization andsubsequent condensation of the foamed oil.

The condensed oil is then fed into an oil circulation tank (60) througha level control valve. From the oil circulation tank (60), the oil maybe recirculated to the input of the heating coil (20) by a vertical canpump (70). In various embodiments, the vertical pump (70) may pump atapproximately 10 gallons per minute (gpm) to 750 gpm. In variousembodiments, the vertical pump may pump at approximately 100 gpm to 500gpm. In certain embodiments, the vertical pump may pump at approximately300 gallons per minute. The vertical pump (70) may include a cast ironbowl (72), stainless steel wear ring (74), and bronze impeller (76), asshown in FIG. 3. The vertical pump (70) may also be used to create aneddy current (DC), thereby subjecting the oil stream to electrolysiswithout additional power sources. Thus, the eddy current created by thevertical pump (70) provides for modification of the electronegativecharacteristics within the oil stream.

From the oil circulation tank (60), the oil may also flow through asintered stainless tube (80) and into a cooling chamber (90). Withoutbeing bound by theory, the positive charge of the sintered stainlessmakes it possible to change the electrical polarities or pulsepositive/negative current in the oil, thereby disrupting theelectromagnetic field that holds the oil molecules together. As such,the sintered metal provides additional electrical influence to the oilstream without the need for additional power sources. As shown in FIGS.4A and 4B, the heated oil is cooled in cooling chamber (90) by contactwith the plurality of cooling tubes (92) disposed within the coolingchamber (90). The cooling chamber (90) may be further used to slow downmolecular movement of the oil stream (94), thereby increasing andaccelerating crystallization and pairing/gathering of halogens. Withoutbeing bound by theory, the resulting reduction in DC voltage within theoil stream urges separated elements (i.e., halogens) back to theircrystalline (i.e., salt) state. In various embodiments, the coolingchamber (90) cools the oil to approximately 72° F.-80° F. In variousembodiments, the cooling chamber (90) cools the oil to approximately 72°F.-75° F. In certain embodiments, the cooling chamber (90) cools the oilto approximately 73° F.

After being cooled, the oil passes through an electrifier (100) whereinthe oil is subjected to electrical treatment. As shown in FIGS. 1 and5A, a DC power supply creates a short-lived electrical DC currentthrough sintered metal wiring (105) disposed therein. The electricalcurrent creates polar instability within the oil stream, therebycreating atomic shell wobble, as shown in FIG. 5B. Without being boundby theory, because the DC current flows through sintered metal, thecurrent may travel in many directions within the oil stream, therebycreating a pulsing electromagnetic field. The electromagnetic pulsechanges the shape of the atomic shells and subshells of the oilmolecules. When the orbit of the electrons is elongated by thecontrolled electrical pulse, electrons are able to drop out of theirorbit, thereby changing the atomic structure of the molecule.

In certain embodiments, a 0-90 volt electrical field is produced throughsintered copper in the system. In other embodiments, a 0-250 voltelectrical field is produced through sintered titanium in the system.The oil is then collected in a gathering chamber (110) to smooth theflow of oil. The gathering chamber (110) may include an input tube (112)of a first diameter (d1) and an output tube (114) of a second diameter(d2), where the first diameter (d1) is smaller than the second diameter(d2) in order to convert the inputted turbulent flow of the oil intolaminar flow. In various embodiments, the first diameter may beapproximately one inch to 5 inches, while the second diameter isapproximately 6 inches to 12 inches. In certain embodiments, the firstdiameter may be two inches, while the second diameter is approximatelyeight inches.

The gathered oil is then filtered through a filter bank (120) to removecrystallized non-metal elements, such as halogens, from the used oil. Invarious embodiments, the filter bank (120) may be a 900 gpm filter bankcontaining 1-20 micron filter bags. The filtered oil may then becollected for future use through output tube (130) (denoted at “oil out”in FIG. 1). When the treated oil is used or burnt, it does not createdioxin, and yields an oil product having 50% to 90% of the sulfurremoved therefrom.

In another aspect, the present invention provides a method of treatingoil. As discussed above, the treated oil does not create dioxin, and has50% to 90% of the sulfur removed therefrom. The method includes heatingoil in need of treatment to approximately 82° F.-100° F. and aeratingthe heated oil to create an oil foam. In various embodiments, thetemperature is raised to approximately 85° F.-90° F. In certainembodiments, the temperature is raised to approximately 88° F. Thefoamed oil is then subject to a vacuum to remove the air and condensethe oil. The oil is contacted with sintered stainless steel and cooledto approximately 72° F.-80° F. In various embodiments, the coolingchamber (90) cools the oil to approximately 72° F. to 75° F. In certainembodiments, the cooling chamber (90) cools the oil to approximately 73°F.

The cooled oil is then subjected to an electric field. As describedabove, the electric field may be a 0-90 volt DC electrical fieldproduced through sintered copper. In other embodiments, the electricfield may be a 0-250 DC volt electrical field produced through sinteredtitanium. The flow of the electrified oil is then smoothed by passingthe oil through a gathering chamber. Finally, the electrified oil isfiltered to remove crystallized halogens and/or sulfur. In variousembodiments, the electrified oil may be filtered through a 900 gpmfilter bank containing 1-20 micron filter bags. The filtered oil maythen be collected for future use.

Although the invention has been described with reference to the aboveexample, it will be understood that modifications and variations areencompassed within the spirit and scope of the invention. Accordingly,the invention is limited only by the following claims.

What is claimed is:
 1. A method of treating oil comprising: (a) heatingoil; (b) aerating the heated oil to create an oil foam; (c) subjectingthe oil foam to a vacuum to condense the oil; (d) contacting thecondensed oil with a sintered metal; (e) cooling the condensed oil; (f)subjecting the cooled oil to an electrical field; and (g) filtering theelectrified oil.
 2. The method of claim 1, wherein the oil is used oil.3. The method of claim 1, wherein the oil is heated to about 82° F.-100°F.
 4. The method of claim 3, wherein the oil is heated to about 88° F.5. The method of claim 1, wherein the step of aerating includescontacting the oil with a plurality of nitrogen diffusers while pumpingair through the diffusers.
 6. The method of claim 1, wherein thesintered metal is sintered stainless steel.
 7. The method of claim 1,wherein the oil is cooled to about 72° F.-80° F.
 8. The method of claim7, wherein the oil is cooled to about 73° F.
 9. The method of claim 1,wherein the electrical field is a 0-90 volt electrical field is producedthrough sintered copper.
 10. The method of claim 1, wherein theelectrical field is a 0-250 volt electrical field is produced throughsintered titanium.
 11. The method of claim 1, wherein the electrifiedoil is filtered using a 1-20 micron filter bank.
 12. A system fortreating oil comprising: (a) a line for inputting oil; (b) a heatingcoil having an input and an output, wherein the input is in fluidcommunication with the line, and the heating coil is configured forheating the inputted oil; (c) an air injection passage in fluidcommunication with the output of the heating coil, the air injectionpassage comprising a plurality of sintered metal injectors configured toaerate the heated oil; (d) a vacuum chamber in fluid communication withan output of the air injection passage, and configured to condense theaerated oil; (e) a cooling chamber in fluid communication with an outputof the vacuum chamber, and configured to cool the condensed oil; (f) achamber containing sintered metal in fluid communication with an outputof the cooling chamber; (g) an electrifier in fluid communication withan output of the chamber containing sintered metal, and configured tosubject the cooled oil to an electrical field; and (h) a filter bank influid communication with an output of the electrifier, and configured tofilter the electrified oil.
 13. The system of claim 12, wherein the oilis used oil.
 14. The system of claim 12, wherein the heating coil isconfigured to heat the inputted oil to about 82° F.-100° F.
 15. Thesystem of claim 14, wherein the heating coil is configured to heat theinputted oil to about 88° F.
 16. The system of claim 12, wherein the airinjection passage further comprises a plurality of nitrogen diffusers incontact with the heated oil.
 17. The system of claim 12, wherein thecooling chamber is configured to cool the oil to about 72° F.-80° F. 18.The system of claim 17, wherein the cooling chamber is configured tocool the oil to about 73° F.
 19. The system of claim 12, wherein thesintered metal is sintered stainless steel.
 20. The system of claim 12,wherein the electrifier comprises sintered copper in contact with thecondensed oil, and is configured to generate a 0-90 volt electricalfield through the sintered copper.
 21. The system of claim 12, whereinthe electrifier comprises sintered titanium in contact with thecondensed oil, and is configured to generate a 0-250 volt electricalfield through the sintered titanium.
 22. The system of claim 12, whereinthe filter bank comprises a 1-20 micron filter.